Raw Material Required by Marble Industries
The marble industry is a small-scale industry. Before 2010, they were observing 2 to 3 shifts per day of 8 hours each. Due to the war on terror, the duty hours were decreased. After 2014 and onwards, the number of shifts has been decreased to one shift with 8 to 12 working hours per day. It has decreased the production rate of industries by 30–40%. Other reasons for reduced working hours and low production are the insecure environment (terrorism) and the lack of skilled labor. Marble stone is used as the basic raw material. It is required in the range 10000–18000 Kg per day by each industry (Table-2). The raw material comes from the regions neighboring Peshawar, including the areas of Mardan, Swabi, Buner and Hazara. It is supplied by the contractors to the industries. Thelarge vehicle (truck, traila) is used to bring the raw material. Water is another important input used in the manufacturing of marble. The daily intake of water consumption is 1700 to 2500 m3 per industry (Table-2). The source of water is groundwater. Each industry has its own source of underground water. Plastic and paper are the minor raw materials required for packing.
Output generated by Marble Industries
The marble processing industry is a resource- intensive and a regular source of pollution. Besides the product, waste is produced that is classified as by-product or waste. The production rate of 6 marble industries is calculated between 8500 to 15500 Kg/day (Table-2.) Waste is generated in the form of gravels and damaged slabs, slurry and sludge, dust, wastewater, oil and lubricants as discussed below;
Solid Waste generated by Marble Industries
As marble stone is the main input of the industry, therefore, it undergoes various steps to make the final product. Table-2 shows the quantity of waste determined for the marble processing industries. In Addition to wastewater, the marble industries also contribute a large part to the production of solid waste in the order of 1500 to 2500 Kg/day. This waste comes in the form of sludge and waste-marbles. The damaged marbles are sold to the community for construction while the sludge is dumped openly on the roadside or in the nearby areas. Marble waste is a good raw-material in the preparation of secondary products. By using it as a raw-material, this will help to protect the environment and would be cost-effective. During the field visit, waste handling and its management was identified as the most serious problem for industries and their environment. But no one intends to launch efforts to alleviate this problem and to hand over the responsibility of managing environmental problems to the government.
On the other hand, the lack of government incentives was also seen as ineffective. Due to the lack of treatment facilities, dumping sites and recycling systems for industrial solid waste, people have to face an unhealthy environment. This mismanagement of solid waste opens a pathway for environmental pollution, posing adverse effects on the environment and humans. Marble slurry is rich in CaCO3 that affects life and block the main drains and channels thus causing drainage problems (Al-Joulani, 2012). To overcome the environmental problems, Pakistan took the first step in 1983 in the form of Environmental Protection Ordinance (PEPO) with the help of Environmental Protection Agencies (EPAs) to formulate the Pakistan Environmental Protection Act,1997 (PEPA). For all developmental and manufacturing activities, Environmental Protection Assessment (EIA) was considered mandatory under section 12 of PEPA-1997. EPA proposed monitoring rules and IEE/EIA regulations and considered it mandatory for small and large scale industries such as sugar, steel, cement and marble industries etc. As marble processing industry is a large scale industry and it needs at least 10 million budget for its installation, therefore, the EPA developed an environmental checklist (EAC) in 2004 (Shah, 2011). Furthermore, national guidelines and permissible safe limits were formulated for industrial discharges by the Pakistan Environmental Protection Agency under clause (d) of Section (6) of the Pakistan Environmental Protection Ordinance with the approval of the Pakistan Environmental Protection Council. They established the National Environmental Quality Standards (NEQS) in 1993 for the air, water and soil (PEPC,1995: JICA, 2003).
Table-2 Solid Waste Produced by Marble Industries at Hayatabad Industrial Estate
Industry | Raw material consumption (Kg)/day | Waste (Kg)/day | Product (Kg)/day | Water Consumption m3/day | Wastewater m3/day | Energy Utilized kWh/month |
Marble-1 | 10000 | 1500 | 8500 | 37 | 30 | 16820 |
Marble-2 | 10000 | 1520 | 8480 | 40 | 33 | 17211 |
Marble-3 | 12000 | 1540 | 10460 | 46 | 40 | 20123 |
Marble-4 | 13000 | 1600 | 11400 | 51 | 44 | 23010 |
Marble-5 | 15000 | 1700 | 13300 | 57 | 52 | 25213 |
Marble-6 | 18000 | 2500 | 15500 | 66 | 60 | 27264 |
Energy Consumption
The main source of energy utilized in the marble industries is the electric source. The consumable energy was estimated from monthly bills. The monthly units of consumable electricity for each industry were noted in the range of 16820 to 23010 kWh (Table-2). A considerable amount of energy is used by the marble industries; therefore, each industry installed its separate transformer of about 200 KVA. It was observed during the investigation that the cutting and polishing steps acquire a greater amount of energy. No fuel-burning practice was observed in any industry which, in turn, can help to minimize the environmental impacts generated form energy consumption sources. While Natural Gas is only used for heating and cooking purposes. The only source of energy in the marble industries is grid-supplied electricity.
Oil and Lubricants
During marble manufacturing, oil and lubricants are produced in cutting units, polisher and wheelbarrows. These wastes are considered as hazardous waste and need proper management. But industries lack such practice and they throw lubricants into the main industrial drain. This practice is a big threat to the aquatic biota of receiving water channels.
Plastic and wood
These are minor waste and used as complementary material, holding and packing of marble. As per day estimation, plastic and wood are produced up to 10–15 kg. It is given free of charge to workers or scavengers for burning purposes.
Dust (Air Pollution): Dust has been found emitting during material handling, cutting and polishing of marbles. It was observed to be deposited 3–4 cm on the land surface. This dust has been considered as the main environmental concern of marble manufacturing. This dust poses harmful effects on soil quality, plant growth, water quality, animal and human health. Marble dust has several industrial uses because it contains a high percentage of fine particles and a low percentage of metal oxides. The literature revealed that the calcareous particles of ultra-fine size can be well recovered and then marketed for numeral industrial applications which employ micronized calcium carbonate. These include: the production of cement, paint, paper, soda, lime, agricultural soil amendment, acid neutralizer for heavy metal sorption and industrial discharges desulphurization of flue gas in electric power stations (Misra & Gupta, 2008: Pincomb & Shapiro, 1994). To avoid the harmful effects of dust, no control strategy as observed. Out of the six marble processing units, only 1 plant was observed with medium wet processing. To minimize pollution at source, the UN Environment Program introduced the idea of Cleaner Production (CP) to Pakistan’s industrial sector in 1994 (Ozbay and Demirer, 2007). It is a preventive technique to reduce harmful impacts on the environment by applying environmental regulations. By adopting such techniques, less harmful pollutants are generated (Frondel et al., 2007). Unfortunately, these practices are not adopted due to poor laws.
Noise: During marble manufacturing, noise was monitored in marble industries. The highest noise was noted at the point of noise source above the safe limit in the range of 92–98 dB (Figure-1). While the lowest noise was measured a distance of 50 meters from the source varied from 33–44 dB (Figure-1). According to Pak-NEQS, the proposed permissible limit of industrial noise is 75–80 dB (PEPC, 1995). This limit has been recommended as a draft on the national standard of noise. This draft has been prepared by Pakistan Environmental Protection Council in 1995 which is not approved yet but is applicable. Based on the results, the loud sound poses harmful effects on the eardrums of workers and the people living nearby the factories. Therefore, industrial colony/residential area should be at least 100 m away from noise creating factories. At present, there are no national standards in Pakistan to prescribe noise limits for the industry. Therefore, the EPA don not take action and thus industries are free and not serious to control it. It is, therefore, important to pass the noise pollution control law and the creation of a high level and unnecessary noise has to be prohibited with strict punishment under the law of PEPO,1983. Literature surveys in Pakistan have revealed noise as the silent killer of humans. This issue is increasing from zone to zone and varied according to emission source (Tajik, 2001: Shaukat, 2002: Irfan, 2002: Mehdi et al, 2002).
Fig-1: Noise generated by Marble industries in dB.
Wastewater Characteristics of Marble Industry
The marble industries generate complex wastes in the form of wastewater and marble slurry. Marble cutting and polishing needs water for cooling purposes. As a result, a huge amount of suspended solids is produced (Fig-2). Analysis of wastewater of marble industries showed a heavy load of suspended solids with the average range of 18575–19930 mg/L. This level is higher than Pak-NEQS (150mg/L) and is a major source of water pollution. The regulatory measures of the NEQS do not allow any industry to discharge effluents with TSS concentrations above the safe limit (150mg/L) into a receiving water channel. Therefore, the marble industries must operate the sedimentation tanks to keep the TSS level low before discharging the effluents into a freshwater body.
Fig-2: Physicochemical parameters of wastewater of marble industries.
Turbidity has been identified as the second factor indicating water pollution in marble wastewaters. The average values were recorded between 340–455 NTU. Water rich in TSS will have higher turbidity and low clarity (Shah, 2011). While other parameters such as pH. EC, Alkalinity, TDS, BOD5 and COD were within the allowable limits (Fig-2). Analysis of heavy metals showed that all metals were found below their permissible limits (Fig-3).
Fig-3: Concentrations of Heavy metals in wastewater of marble industries.
For water reuse, the effluents can be deposited settling ponds. The water is recirculated for cooling. The resulted sludge, also called marble slurry is discarded (Aukour et al., 2008). After recycling the wastewater for 2–3 times, it cannot be reused and is therefore discharged into a nearby stream/river. The existing mechanism in marble units found ineffective in term of recovering the marble slurry. Wastewater from industries is not monitored properly and is discharged into nearby water channels. These discharges contain toxic pollutants that show their significant responses to the aquatic ecosystem. A great diversity of pollutants leads to several disorders (Shah, 2011).
ANOVA test results showed significant differences for pH, EC, TDS, TSS, BOD5 and COD. While for heavy metals, the test results of ANOVA were insignificant (Table-3). The manufacturing of marble poses several environmental problems, in particular the quality of the water for safe cutting and shaping steps is of great importance. Therefore, the water used in the marble industry needs to be of good quality without containing suspended load (Domopoulou et al., 2015).
Table 3
ANOVA Test for Wastewater Parameters of Marble Industry Dependent Variable: data
Type | Dependent Variables | Sum of Squares | Df | Mean Square | F-value | Sig. |
Wastewater Parameters | Between Groups | 12670410.006 | 7 | 2473902.217 | 150.328 | .001 |
Within Groups | 3425276.400 | 102 | 10428.506 | | |
Total | 26170651.370 | 106 | - | - | - |
Heavy Metals in wastewater | Between Groups | 112.016 | 7 | 50.018 | 128.417 | .120 |
Within Groups | 11.872 | 130 | .127 | | |
Total | 166.022 | 131 | | | |
Construction of settling tank is mandatory under Environmental Impact Assessment (EIA) regulations 2000. In Hayatabad Industrial Estate, each marble industry has constructed the sedimentation tanks, but most of the them are not operational. Another possibility to construct one big sedimentation tank for all marble processing units.
Another problem in waste management is the improper location of marble processing units. Marble industries are scattered out through whole industrial estate and therefore, need a separate sector to relocate. It will cost a single industry $ 3–4 million to install it in a new location. If industries are brought in one zone, they will throw their discharges into the same drain that will be helpful to collect the sludge from one specific site. Marble waste is rich in calcium carbonate contents and is used as an important raw material in the preparation of cement, washing powder and tiles. Therefore, these industries should be kept in one zone. Furthermore, it is possible to install a combine treatment plant near the marble industries to recycle their wastewater. This will reduce the pollution load of the industrial estate which is economically viable and environmentally friendly. The cement and ceramic industries depend on marble waste and therefore, must be placed near the marble industry.
Treatment of Marble Wastewater
For wastewater utilization, wastewater from the marble industry was treated in the laboratory under two stage treatment techniques, i) sedimentation, ii) coagulation. For this purpose, the wastewater from an industry (marble-6) was selected as given below
Wastewater of Marble Industry after Primary Sedimentation. Selected samples of wastewater from marble industries after primary sedimentation showed a gradual change in the physicochemical characteristics, the average pH being noted as 7.2. The level of suspended solids and turbidity were depressed to 33% and 32% respectively (Table-4). The literature has shown that sedimentation is an effective method for the removal of suspended solids (Thompson et al., 2001: Khan et al., 2016). BOD5 and COD were depressed up to 19% and 14% respectively. Comparative t-tests for untreated and treated samples under the sedimentation process showed significant differences as < 0.05. In case of multiple comparisons, highly significant differences were observed among pH to EC, TSS, BOD5 and COD. While BOD5 was found insignificant to COD (Table-5). Marble sludge after recycling is applicable for use as whitewash, in paint, as a filler in concrete, electric insulator and industrial filters (Industrial Minerals HandyBook, 2002). All of these applications provide valuable options from a waste material. Considerably, the most effectual and widely applicable way is using the waste in civil and mining engineering works. (Siotto et al., 2008). In the literature review Arel (2016) and Shah (2015), the examined studies focused on the waste marble use for replacing cement and its cumulative form in concrete production. In our study, no practice of waste reuse or waste sharing was observed in any industry. They disposed of the waste openly which is a big environmental concern for the industrial area.
Table 4
Sedimentation Test Results for Wastewater of Marble Industry
Parameter | Marble Industry-6 |
Min | Max | Avg | SD | Removal (%) |
pH | Before | 7.4 | 8.1 | 7.8 | 0.34 | -- |
After | 7.1 | 7.4 | 7.2 | 0.11 |
EC uS/Cm | Before | 824 | 912 | 890 | 9.01 | -- |
After | 752 | 801 | 769 | 4.31 |
Alkalinity mg/L | Before | 614 | 675 | 644 | 3.42 | -- |
After | 477 | 534 | 518 | 2.81 |
Turbidity NTU | Before | 411 | 489 | 455 | 3.01 | 32 |
After | 288 | 344 | 310 | 2.71 |
TDS mg/L | Before | 554 | 605 | 580 | 3.12 | 12 |
After | 487 | 540 | 512 | 3.00 |
TSS mg/L | Before | 23606 | 25045 | 24130 | 11.02 | 33 |
After | 15855 | 18002 | 16236 | 9.14 |
COD mg/L | Before | 90 | 133 | 102 | 2.46 | 14 |
After | 74 | 96 | 88 | 2.23 |
BOD5 mg/L | Before | 34.5 | 62 | 48.5 | 1.12 | 19 |
After | 29.5 | 46.5 | 39 | 1.05 |
Table 5 ANOVA Test Results for Sedimentation Treated wastewater Dependent Variable: data
Source | Type II Sum of Squares | Df | Mean Square | F-value | Sig. |
Model | 64135676.225a | 8 | 4432122.241 | 126.346 | .000 |
Parameters | 41414234.024 | 7 | 6535642.123 | 233.604 | .000 |
treated/untreated | 1530418.346 | 1 | 1530417.346 | 43.446 | .000 |
Error | 2305864.764 | 103 | 300228.126 | | |
Total | 47643648.340 | 112 | | | |
a. R Squared = .916 (Adjusted R Squared = .932) |
Wastewater after Treatment with Coagulation
To remove the suspended load and improve the wastewater quality of marble industries, different coagulants have been applied. The pH was adjusted by keeping it within the permissible limit of Pak-NEQS. In treated samples, the values of electrical conductivity and TDS were observed high due to the addition of coagulants. The average values for removable suspended solids ranged between 68% and 92% after coagulation. The highest removal of suspended load was observed with coagulant FeCl3.6H2O (92%) with minimum settling time (22mints). Al2(SO4)3.18H2O also showed efficient results for the removal of pollution load from marble wastewater with 79% of TSS removal. While the lowest removal of suspended load was observed with FeSO4.7H2O (68%), shown in Fig-4. pH is an important indicator for water and therefore, is closely associated with the coagulation process. The pH values remained within the safe limit during treatments of FeCl3.6H2O and Al2(SO4)3.18H2O.
Fig-4: Effects of Coagulants on Removal of TSS.
In case of FeSO4.7H2O, the pH turned into acidic as 4 to 5.5. Therefore, the Alumina and Ferric chloride found effective for maximum removal of pollutants resulting in low water turbidity. Turbidity is also an important water parameter which determines the presence of colloidal particles. Water with higher colloidal particles show higher turbidity. The colloidal particles have negative surface charges resulting from repulsion forces that exist between particles. To destabilize these particles, it is important to add cationic chemical reagents such as coagulants. During treatment, a decrease trend of settling time was noted with increasing doses of coagulants due to declining of colloidal particles. During coagulation, small molecules combine to form flocks that settle down because of their weight (Kumar et al., 2011). The physicochemical parameters of untreated and treated water samples were found highly significant to each other (< 0.05). While multiple comparisons of water parameters showed significant associations of pH to EC, TSS and COD.
Settling Time
The effect of settling time was noted for the removal of suspended solids. For sedimentation, the observed time was 24hours. In coagulation, the operating time was dependent on the coagulant dose as the settling time was reduced with increasing dosage of coagulants. The. The minimum removal of suspended solids was obtained with 10ml of coagulants. The other doses were applied as 20, 30, 40, and 50ml. Maximum removal of suspended solids (92%) was observed with 50ml of Ferric chloride. For this, the time observed was 52, 43, 29, and 22 minutes.
Literature revealed that coagulation is one of the efficient treatments for the wastewater of the marble industry. Arsalan et al., (2005) reported that coagulation with Alum (Al2SO4)3) and FeCl3 were considered capable of maximum removal of turbidity and suspended solids.
Aguilar et al., (2002) explored the effective results of coagulation treatment on wastewater of marble industry and reported that coagulation treatment is important for the removal of suspended materials. Semerjian and Ayoub (2003) investigated that coagulation has got much attention for the maximum, removal of pollutants from the wastewater of the marble industry. The presence of lime and carbonates increase the pH and thus lead to water clarification. Domopoulou et al., (2015) reported the effective results of coagulants (Al2(SO4)3, FeCl3 and FeSO4 for the removal of suspended solids from the wastewater of the marble industry. This treatment was very efficient with 92% results. Literature revealed that the wastewater from marble processing industry is possible and profitable.
Correlation Between Wastewater Parameters
The results of Pearson correlation among wastewater parameters showed a strong association between pH and EC (r = 0.801), turbidity (r = 0.814), TSS (r = 0.822), BOD5 (r = 0.836) and COD (r = 0.845). A strong correlation was observed between TSS-BOD5 (r = 0.851) and TSS-COD (r = 0.860). The correlation between BOD5-COD was observed as r = 0.614 (Table-6). The strong correlations showed that these parameters are dependent on each other for their high and low levels.
Table-6: Pearson Correlation among Wastewater Parameters.
Parameters | Ph | EC | Alkalinity | Turbidity | TDS | TSS | BOD5 | COD |
pH | 1 | |
EC | 0.801* | 1 | |
Alkalinity | 0.743 | 0.788 | 1 | |
Turbidity | 0.814* | 0.754 | 0.650 | 1 | |
TDS | 0.806* | 0.812* | 0.756 | 0.842* | 1 | |
TSS | 0.822** | 0.789 | 0.788 | 0.850* | 0.829* | 1 | |
BOD | 0.836* | 0.765 | 0.794 | 0.836* | 0.774 | 0.805* | 1 | |
COD | 0.845** | 0.788 | 0.782 | 0.759 | 0.746 | 0.822* | 0.644 | 1 |